USPatentGranted
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Process for the purification of mandelic acid N,N-diethylamide

Granted 22 Sep 1992 · no office action yet

Application
649401
filed 1 Feb 1991
Publication
Not published
not published
Patent· this page
US 5,149,873
granted 22 Sep 1992

Life of the patent

2 dated events
⤢ drag to zoomJan 1991Apr 1991Jul 1991Oct 1991Jan 1992Apr 1992Jul 1992Oct 1992Prosecution
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Abstract

A process for the purification of mandelic acid N,N-diethylamide, DEM, by forming a crystalline adduct of DEM with a calcium halide and water.

Description

8 parts
›The present invention relates to a process for…

The present invention relates to a process for the purification of mandelic acid N,N-diethylamide, abbreviated DEM herein. This compound ##STR1## and related mandelamides are useful as insect repellents as described in the Swedish Patent 409808 (1979) to W. Thorsell et al.

The synthesis of DEM can be performed by a 4-step route such as described in the above Swedish patent. Whatever the method of synthesis it is important that the crude DEM obtained is upgraded to obtain a purified material suitable for application to the skin.

The purification of DEM is difficult due to:

a) the very high boiling point and the poor thermal stability, which combine to make fractional distillation very difficult on an industrial scale;

b) the low melting point of DEM, 27°-30° C., and the high viscosity, which make it difficult to crystallize DEM.

It is therefore an object of the present invention to provide a process whereby DEM can be purified in a practical way on an industrial scale using ordinary standard equipment.

The essence of the present invention lies in the surprising discovery that DEM forms crystalline, high-melting adducts with calcium halides and water. Preferred halides are selected from chloride and bromide, and embodiments wherein the halide is chloride are particularly preferred.

More specifically, we particularly prefer two different adducts with the compositions DEM·CaCl 2 ·2H 2 O and DEM·CaCl 2 ·6H 2 O, respectively.

Any of such adducts of DEM with calcium halides and water can be used in the purification of DEM by crystallization.

The novel adducts according to the invention are stable in the presence of sufficiently hydrophobic non-polar or moderately polar solvents such as hydrocarbons, ethers and esters. Solvents of these types are therefore useful crystallization media and will serve to dissolve the impurities that are to be removed.

Although the present invention covers any adducts with calcium halides and water the invention will be illustrated in the following mainly with reference to adducts with calcium chloride and water.

The crystallization of DEM as the adduct with 2H 2 O can be performed by stirring the calculated amount of CaCl 2 ·2H 2 O with a solution of DEM in a solvent. The CaCl 2 ·2H 2 O will dissolve due to adduct formation and DEM·CaCl 2 ·2H 2 O will then crystallize rapidly from the solution.

In a modified procedure a hydrophilic solvent such as water or a lower alcohol is added to redissolve the DEM·CaCl 2 ·2H 2 O or to prevent it from precipitating too rapidly. The crystallization may then be completed by distilling off the hydrophilic solvent.

The adduct with 6H 2 O can be crystallized by contacting a solution of DEM in a sufficiently hydrophobic solvent with an approximately 50% aqueous solution of CaCl 2 , corresponding to CaCl 2 ·6H 2 O. When the two essentially immiscible solutions are stirred together, crystals of DEM·CaCl 2 ·6H 2 O will start forming. The process is typically performed at room temperature and the crystallization takes place at a convenient rate if moderate stirring is applied. A high yield of good crystals can thus be obtained in as little as one half hour, although stirring is preferably continued for one or a few hours.

The crystals of DEM·CaCl 2 ·2H 2 O or DEM·CaCl 2 ·6H 2 O thus obtained are typically almost colourless. They are separated from the coloured mother liquor by filtration or centrifugation and washed with solvent. Purified DEM is then set free by stirring the crystals, normally in the presence of adhering solvent, with a suitable amount of water. DEM, together with any solvent, is obtained as an oil phase that separates from the aqueous phase containing the calcium chloride.

After collecting the DEM phase any traces of calcium chloride are removed by extracting with water. Evaporation of solvent leaves DEM of high purity.

The present invention will now be further exemplified by non-limiting examples.

›Examples7
›EXAMPLE 1

Preparation of DEM·CaCl 2 ·2H 2 O adduct

DEM (41 g=0.2 mol) was dissolved in toluene (163 ml). While stirring at 45° C., finely crystalline CaCl 2 ·2H 2 O (22.1 g=0.2 mole) was added. The calcium chloride dissolved rapidly but before dissolution was complete a new precipitate started to form. After stirring for 15 minutes this was filtered off with suction. 64 g of moist crystals were obtained.

›EXAMPLE 2

Preparation of adduct with recrystallization

A slurry of adduct in toluene was prepared as in Example 1. Ethanol (88 ml) was added and the temperature was raised to about 90° C. to dissolve the crystals. The ethanol was then slowly distilled off, whereby the adduct crystallized in a purified form.

›EXAMPLE 3

Preparation of DEM·CaCl 2 ·6H 2 O

The formation of this adduct was demonstrated with crude DEM of 95% purity:

Crude DEM (50 g=0.229 mol) was dissolved in ethyl acetate (116 ml). CaCl 2 ·2H 2 O (32.0 g=0.217 mol) was dissolved in water (15.7 g=0.870 mol) at 40° C. The two, essentially immiscible solutions were stirred together. After about 15 minutes crystals started to form in the aqueous phase and after another 15 minutes the crystallization was complete. The resulting slurry of crystals in ethyl acetate was filtered to give 79 g of almost colourless adduct.

›EXAMPLE 4

Preparation of DEM·CaCl 2 ·6H 2 O

The process of Example 3 was repeated but with toluene, butyl acetate or isobutyl acetate instead of ethyl acetate. All these three solvents gave a yield of about 85 g of almost colourless adduct.

›EXAMPLE 5

Recovery of Purified DEM by Hydrolysis of DEM·CaCl 2 ·6H 2 O

10.0 g of the adduct from Example 3 was stirred with 10.0 g water for 15 minutes at 30° C. The lower phase, containing calcium chloride in water, was then separated from the organic phase. The latter was washed with water to give 4 g of DEM as an almost colourless oil.

›EXAMPLE 6

Recovery of Purified DEM by Hydrolysis of DEM·CaCl 2 ·6H 2 O

10.0 g of the adduct from Example 3 was stirred with 5.0 g water and 5 g ethyl acetate. After stirring for 15 minutes at 30° C., the lower phase, consisting of a 25% solution of calcium chloride in water, was separated from the organic phase. The latter was washed with water and evaporated to give 4.5 g of DEM as an almost colourless oil that crystallized on standing.

›EXAMPLE 7

Preparation of DEM·CaBr 2 ·2H 2 O adduct

In a beaker with stirring there was charged in the order given:

DEM 10.62 g=0.0513 mol

Toluene 50 ml

CaBr 2 ·H 2 O 11.68 g=0.0513 mol CaBr 2 and 0.076 mol H 2 O (11.7% water)

Water 0.42 g=0.023 mol

On heating to 65°-70° C. the calcium bromide dissolved. Before dissolution was complete a new precipitate of DEM·CaBr 2 ·2H 2 O was formed.

This precipitate was filtered off and was found to dissolve in water with liberation of DEM as an oily phase.

1 of 8 part labels are ours — the grant heads the rest

Claims

9 · 2 independent · depth 6
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9 granted claims

Classifications

4 codes
IPC · International Patent Classification
Section A — Human necessities
  • A01N37/18
Section C — Chemistry; metallurgy
  • C07C231/24
  • C07C235/34
USPC · US Patent Classification
564/170

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Pendency
1.6 y
599 days filing → grant
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Examiner
Carolyn Elmore
art unit 129 · TC 1200
Citations: 3 back · 3 forward

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Worldwide family

13 members · 9 offices
US1EP2JP1AT1DE2DK1ES1GR1SE3
this patentIP5 & PCTother officessolid = grantedhover for detail · click to open
Members
13
DOCDB simple family 20378469
Offices
9
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Granted
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Non-English titles
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›IP5 & PCT — 4 members
OfficePublicationKindPublishedFiledStatusTitle
USthis patentUS-5149873-AA22 Sep 19921 Feb 1991grantedProcess for the purification of mandelic acid N,N-diethylamide
EPEP-0441760-A1A114 Aug 19914 Feb 1991publishedReinigungsprozess für N,N-Diethylmandelsäureamidde
EPEP-0441760-B1B111 Jan 19954 Feb 1991grantedReinigungsprozess für N,N-Diethylmandelsäureamidde
JPJP-H072749-AA6 Jan 19955 Feb 1991publishedマンデル酸n,n−ジエチルアミドの精製法ja
›Other offices — 9 members
OfficePublicationKindPublishedFiledStatusTitle
ATAT-E116965-T1T115 Jan 19954 Feb 1991grantedReinigungsprozess für n,n-diethylmandelsäureamid.de
DEDE-69106538-D1D123 Feb 19954 Feb 1991grantedReinigungsprozess für N,N-Diethylmandelsäureamid.de
DEDE-69106538-T2T218 May 19954 Feb 1991grantedReinigungsprozess für N,N-Diethylmandelsäureamid.de
DKDK-0441760-T3T312 Jun 19954 Feb 1991grantedFremgangsmåde til rensning af N,N-dimethylmandelsyreamidda
ESES-2066413-T3T31 Mar 19954 Feb 1991grantedProcedimiento para la purificacion de n,n-dietilmandelamida.es
GRGR-3015020-T3T331 May 19958 Feb 1995publishedPurification process for N,N-diethylmandelamide.
SESE-9000421-D0D06 Feb 19906 Feb 1990publishedPurification processsv
SESE-9000421-LL7 Aug 19916 Feb 1990publishedReningsfoerfarandesv
SESE-502756-C2C28 Jan 19966 Feb 1990publishedFörfarande för rening av mandelsyra-N,N-dietylamidsv

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